EP1761567A1 - Processing of cassava - Google Patents
Processing of cassavaInfo
- Publication number
- EP1761567A1 EP1761567A1 EP05749454A EP05749454A EP1761567A1 EP 1761567 A1 EP1761567 A1 EP 1761567A1 EP 05749454 A EP05749454 A EP 05749454A EP 05749454 A EP05749454 A EP 05749454A EP 1761567 A1 EP1761567 A1 EP 1761567A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- cassava
- roots
- slurry
- product mass
- grating
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 235000016735 Manihot esculenta subsp esculenta Nutrition 0.000 title claims abstract description 92
- 241000658379 Manihot esculenta subsp. esculenta Species 0.000 title 1
- 240000003183 Manihot esculenta Species 0.000 claims abstract description 91
- 238000000034 method Methods 0.000 claims abstract description 49
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 33
- 239000002002 slurry Substances 0.000 claims abstract description 32
- 235000013312 flour Nutrition 0.000 claims abstract description 23
- 238000001035 drying Methods 0.000 claims abstract description 18
- 102000004169 proteins and genes Human genes 0.000 claims abstract description 12
- 108090000623 proteins and genes Proteins 0.000 claims abstract description 12
- 239000000047 product Substances 0.000 claims description 33
- 229920002472 Starch Polymers 0.000 claims description 27
- 235000019698 starch Nutrition 0.000 claims description 27
- 239000008107 starch Substances 0.000 claims description 27
- 238000005406 washing Methods 0.000 claims description 25
- 238000001914 filtration Methods 0.000 claims description 24
- 239000000706 filtrate Substances 0.000 claims description 12
- 238000005520 cutting process Methods 0.000 claims description 6
- 238000007670 refining Methods 0.000 claims description 6
- 238000012216 screening Methods 0.000 claims description 3
- 238000009991 scouring Methods 0.000 claims description 2
- 239000000306 component Substances 0.000 claims 9
- 241000196324 Embryophyta Species 0.000 description 7
- 238000009434 installation Methods 0.000 description 5
- 210000004027 cell Anatomy 0.000 description 4
- 229910052500 inorganic mineral Inorganic materials 0.000 description 4
- 239000011707 mineral Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 150000002825 nitriles Chemical class 0.000 description 3
- 244000061456 Solanum tuberosum Species 0.000 description 2
- 235000002595 Solanum tuberosum Nutrition 0.000 description 2
- 210000002421 cell wall Anatomy 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 239000013505 freshwater Substances 0.000 description 2
- 239000013067 intermediate product Substances 0.000 description 2
- 235000012015 potatoes Nutrition 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 1
- 241000209140 Triticum Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000016383 Zea mays subsp huehuetenangensis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 235000009973 maize Nutrition 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B30/00—Preparation of starch, degraded or non-chemically modified starch, amylose, or amylopectin
- C08B30/02—Preparatory treatment, e.g. crushing of raw materials or steeping process
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B30/00—Preparation of starch, degraded or non-chemically modified starch, amylose, or amylopectin
- C08B30/04—Extraction or purification
Definitions
- this starch is mainly obtained from potatoes, maize, wheat and cassava. It is in the first place an object of the present invention to provide an improved method for obtaining cassava flour (mainly starch plus fibres) from cassava roots, both as an intermediate product for cassava starch and as a final product, under specific circumstances.
- this method is characterized by grating the cassava roots, adding water to the grated matter to form a slurry, removing undesired components, such as proteins, among other components, from the slurry so as to obtain a product mass and, finally, drying the product mass.
- a method carried out in this manner makes it possible to realize a continuous process for obtaining cassava flour from cassava roots, wherein the method can be carried out locally (i.e. in the immediate vicinity of the production location of the cassava roots), using simple means. This is of major importance, because cassava roots are highly perishable, so that rapid processing is advantageous in that case. As a result, the losses caused by decay are reduced and the processibility is increased.
- Raw material for the preparation of starch can be supplied with a higher degree of reliability. After transportation, the cassava flour can be processed into starch at a suitable location.
- any protein that may be present is prevented from coagulating during the subsequent drying of the product mass and, as a result, enclosing the starch, which could no longer be extracted in that case .
- the present invention is de- scribed herein on the basis of the processing of cassava, but that the scope of the invention is not purely limited to this application, but that it also extends to other tuberous, bulbous or root crops (such as potatoes or batatas) . For the sake of the readability of the description, only cassava is generally mentioned.
- the cassava roots are cut into parts prior to said grating, which parts are subsequently grated. Cutting the cassava roots into parts enhances the effectiveness of the grating process. Furthermore, the addition of water to the grated matter so as to form a slurry preferably takes place during said grating already. This is a highly effective manner of optimising the forming of a slurry already during the grating process and dissolving the undesired components (among which minerals, proteins and cyanides) to a large extent at a later stage during the process and subsequently simply washing them away. The availability of a sufficient amount of water is important in this connection. Chemicals may furthermore be added to the water.
- the removal of undesired components from the slurry so as to obtain a product mass takes place by filtering the slurry, with the product mass as the residue and the water containing the components that are undesired for the flour product as the filtrate.
- a filtering process functions as a pre-drying (dewatering) step of the slurry, as it were, which already has a very high starch content (the moisture content may already have been reduced to about 40% in that case, for example) .
- the filtrate might be used as fertilizer.
- Said filtering can take place (preferably) by means of a vacuum filter, so that a comparatively small water volume will suffice for said washing.
- the minerals and the like are obtained from the root in a relatively high concentration, so that reuse thereof as fertilizer becomes possible (at the lowest logistics costs) . Furthermore it is possible within this framework to wash the residue with clean water, which further helps remove the undesired components.
- the product mass which, as described in the foregoing, has already been (me- chanically) pre-dried (dewatered) , can be dried by means of hot air.
- a so-called vortex dryer or a so-called thorbed dryer
- the product mass swirls around and escapes from the vortex dryer when the eventual product is sufficiently dry.
- the hot air may have a temperature in the 100-140 °C range, with the temperature of the hot air preferably being maximally 120 °C. Also other manners of drying are conceivable, for example drying in the sun.
- the method according to the invention can be further optimised if the filtrate that is formed during the filtration of the slurry is used for washing the cassava roots. It is possible to screen the filtrate before it is used for washing the cassava roots so as to at least largely remove any undesired components therefrom.
- Said peeling of the cassava roots can take place by bringing the cassava roots into scouring contact with each other during the washing process.
- This can be realised, for example, when the cassava is placed in a layer of water and is subsequently set moving. As a result, the outer skin will become detached and can be washed away with the washing water.
- the washing water may be spread over the fields, using suitable means (pumps, hoses, tank trucks, etc) .
- the cassava roots are thus grated while they are fresh, as a result of, which the cells are opened and all the starch that is present is released.
- cassava rods are cut into slices, which slices are dried and subsequently ground into flour.
- a draw- back of such a known method is the fact that not all the starch is released and that the starch is probably severely damaged.
- grating as used within the framework of the present disclosure should be understood to mean any process for dividing/chopping the cassava roots in which the cells thereof are opened; this in contrast to the term “cutting”, which is generally understood to mean a process for dividing the cassava roots in which the cells remain largely intact.
- the invention also relates to a method for refining cassava into starch, wherein the cassava is processed into cassava flour at a first location, which cassava flour is subsequently further processed into starch at a second location.
- said processing of the cassava at the first location takes place by using a method according to the invention as described in the foregoing.
- the present invention also relates to a device therefor.
- such a device is characterized by means for grating the cassava roots, means for adding water to the grated matter so as to form a slurry, means for removing undesired components, such as proteins, from the slurry so as to obtain a product mass and, finally, means for drying the product mass.
- the means for grating the cassava rods consist of rotating cylinders (which may have a diameter ranging between 55 and 85 cm, for example, and which may rotate at a speed of 3000 revolu- tions per minute or at a circumferential velocity of 100 m/s) provided with saw blades.
- the saw blades open the cell walls, causing the starch that is present to be released.
- the saw blades may be comb-shaped grating blades, for example.
- the various means of the device according to the invention may be advantageously mounted on/in at least one standard container, in particular on/in two standard containers. This makes it possible to transport the device from location to location, using locally available means of transport, and to use the device at the locations where the production of cassava takes place. In this framework it is advantageous if the containers are fitted with means by which they can be loaded and unloaded without the use of external aids (cranes, forklift trucks) being required.
- the invention also relates to a device for refining cassava into starch, which device comprises a first part dis- posed at a first location for processing the cassava into cassava flour, and a second part disposed at a second location for processing the cassava flour further into starch.
- the first part of the device is comprised of a device according to the invention as described in the foregoing. It is also preferable in that case if the second part is specially adapted for processing the cassava flour that has been obtained by carrying out the method according to the present invention.
- the device can be optimally adapted for processing the cassava flour, which, as a result of the method according to the invention being carried out, may have a slightly altered structure in comparison with conventionally obtained cassava flour.
- the invention relates to cassava flour and starch obtained by using a method according to the present invention.
- the invention will be explained in more detail hereinafter with reference to the drawing, which shows an embodiment of a device according to the invention.
- the only figure is a schematic side elevation of an embodiment of the device according to the invention placed on two trucks.
- the figure shows two trucks 1 and 2, on which standard containers (or a standard container platforms) 3 and 4 are placed.
- the standard containers can be transported from location to location by means of the trucks 1, 2, where they can be offloaded and be loaded again by an installation (not shown) .
- an installation may form part of the truck 1, 2 or container 3 , 4 in question.
- the trucks 1, 2 or the standard containers 3, 4) are positioned in close proximity to each other and are functionally coupled in a manner yet to be described.
- an energy-generating unit 5 e.g. a die- sel generator
- the energy supplied by said energy generating unit 5 e.g. electric current
- Cassava which is inspected in advance for impurities, the presence of wooden stalk portions and the like, is generally weighed and subsequently carried to a washing in- stallation 7 via a conveyor belt 6.
- the washing installation comprises so-called paddle washers 8 comprising several compartments (e.g. 9 and 10).
- Increasingly clean water is used in the successive compartments for washing the cassava and removing the skin therefrom. Said removing of the skin takes place in that the cassava roots scour against one another in a layer of water.
- a supply pipe 11 is used for supplying washing water. Said supply pipe 11 supplies the washing water from a filtering plant 12, which will be discussed in more detail yet .
- the crops and the peeled cassava roots reach cutting means 15, where the roots are cut into small parts.
- Grating means 16 connect to said cutting means 15 for grating the roots that have been cut into parts.
- the grating means 16 comprise a number of cylinders 17 fitted with projecting saw blades 18, such as comb-shaped grating blades.
- the cylinders have a diameter of 55-85 cm and rotate at a speed of 3000 revolutions per minute. Said rotation of the saw blades 18 opens the cell walls of the cassava roots, so that the starch that is present therein is released.
- a slurry is formed.
- Chemicals may be added to the water as well, for example in order to prevent discoloration or for preservation purposes .
- the cutting means 15 may be left out in another embodiment, so that the grating means 16 connect directly to the washing installation 7.
- the slurry formed in the grating means 16 reaches a trough 21, in which the aforesaid filtering plant 12 is present.
- Said filtering plant 12 com- prises a rotating drum 22, around which a filtering cloth extends.
- the drum 22 has an internal vacuum, as a result of which the slurry is sucked through the filtering cloth from the trough 21.
- the slurry is thereby separated into a fil- trate comprising components that are undesired for certain applications, such as minerals, protein and cyanide, and a residue comprising the product mass 10 to be processed at a later stage.
- Washing water fresh water
- a pipe 23 and possibly atomisers for atomising the added water or the like
- a fixed amount of water per ton of product can be added. This amount may be very low.
- the filtrate water from the filtering plant 12 is supplied to the supply pipe 11 via a discharge pipe 24 and screening means 25 for reuse in the washing installation 7.
- Fresh water may furthermore be added thereto (depending on the use of the product) .
- the eventual water consumption is very low.
- a product mass having a moisture content of ⁇ 40% is obtained in the filtering plant 12.
- the cassava slurry or pulp is subjected to a pre-drying (dewatering) step, as it were.
- the released minerals, proteins and cyanides are washed away to a large extent through the use of the vacuum filter (for example, the protein content of the slurry is reduced from 3% to 0.5% if the raw material is cassava) .
- Any coagulation of protein can be prevented in an effective manner, for example during the drying phase) , thus preventing starch from being enclosed as a result of partial coagulation, so that it can no longer be extracted.
- the pre-dried product mass reaches the second part of the device, which is present on the second truck 2 (or in the container 4) .
- Said second part mainly comprises a so-called vortex dryer 27, in which a drying process is carried out, using hot air (preferably having a temperature of maximally 120 °C) . Residual heat from the energy-generating unit 5 can be used advantageously in the vortex dryer 27 ⁇ (corresponding to 28) . It is noted that it is also possible to use other types of dryers, of course. Of course it is conceivable for the entire device according to the invention to be present inside a single standard container, so that only one truck is needed.
- the distribution of the device over the two standard containers 3 and 4 may furthermore be different from the distribution that is shown herein.
- the number of standard containers may be larger than two, in which case the various components of the device will be suitably distributed over said larger number of standard containers.
- the individual components of the device as shown herein are only examples of possible embodiments. In addition, said components are represented very schematically.
- filtering means that operate in batches (e.g. flat filtering means) might be used. The invention is not limited to the embodiment as described above, which can be varied in many ways within the scope of the invention as defined in the claims.
Landscapes
- Chemical & Material Sciences (AREA)
- Polymers & Plastics (AREA)
- Health & Medical Sciences (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Biochemistry (AREA)
- Fodder In General (AREA)
- Processing Of Solid Wastes (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Non-Silver Salt Photosensitive Materials And Non-Silver Salt Photography (AREA)
- Lubricants (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Drying Of Solid Materials (AREA)
- Confectionery (AREA)
Abstract
Description
Claims
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL05749454.4T PL1761567T5 (en) | 2004-06-09 | 2005-05-30 | Processing of cassava |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL1026370A NL1026370C2 (en) | 2004-06-09 | 2004-06-09 | Cassava processing. |
PCT/NL2005/000393 WO2005121183A1 (en) | 2004-06-09 | 2005-05-30 | Processing of cassava |
Publications (4)
Publication Number | Publication Date |
---|---|
EP1761567A1 true EP1761567A1 (en) | 2007-03-14 |
EP1761567B1 EP1761567B1 (en) | 2011-09-28 |
EP1761567B9 EP1761567B9 (en) | 2012-03-07 |
EP1761567B2 EP1761567B2 (en) | 2016-06-15 |
Family
ID=34969096
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP05749454.4A Not-in-force EP1761567B2 (en) | 2004-06-09 | 2005-05-30 | Processing of cassava |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP1761567B2 (en) |
CN (1) | CN1964991A (en) |
AT (1) | ATE526346T1 (en) |
DK (1) | DK1761567T4 (en) |
NL (1) | NL1026370C2 (en) |
PL (1) | PL1761567T5 (en) |
WO (1) | WO2005121183A1 (en) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101380088B (en) * | 2008-10-16 | 2012-09-05 | 中国农业科学院作物科学研究所 | Production method of cassava food |
US20120003375A1 (en) * | 2010-06-30 | 2012-01-05 | Athula Ekanayake | Cassava Products |
CN102613510A (en) * | 2012-03-22 | 2012-08-01 | 浙江省农业科学院 | Method for processing non-pasted whole tapioca powder |
CN102823831B (en) * | 2012-09-04 | 2013-10-16 | 广西大学 | Edible tapioca flour and preparation method of edible tapioca flour |
US20150315297A1 (en) * | 2012-11-27 | 2015-11-05 | Novozymes A/S | Milling Process |
CN104812778B (en) * | 2012-11-27 | 2019-04-23 | 诺维信公司 | Grinding method |
CN103330111B (en) * | 2013-07-19 | 2015-09-02 | 广西大学 | A kind of method of tapioca starch rapid detoxification |
CN113519589A (en) * | 2021-07-15 | 2021-10-22 | 云南富源金田原农产品开发有限责任公司 | Konjak dietary fiber flaky pastry processing equipment and technology |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE562541A (en) * | ||||
GB256008A (en) * | 1925-06-13 | 1926-08-05 | Samuel William Duncan | Method and apparatus for the manufacture of cassava meal |
US2149802A (en) * | 1938-03-18 | 1939-03-07 | Francis H Thurber | Process for the extraction of root starches |
US2380874A (en) † | 1942-04-20 | 1945-07-31 | Gen Mills Inc | Root starch process |
GB853773A (en) † | 1957-09-30 | 1960-11-09 | Corn Products Co | Starch manufacturing process |
FR1188604A (en) * | 1957-09-30 | 1959-09-24 | Corn Prod Refining Co | Starch manufacturing process |
GB868901A (en) † | 1959-09-18 | 1961-05-25 | Anheuser Busch | Filtration process for starch |
DE2634544A1 (en) * | 1976-07-31 | 1978-02-02 | Ksh Emsland Staerke Gmbh | Starch prodn. without dust formation - by wetting the starting material and immediately wet grinding it before separating the starch |
DE2950315C2 (en) † | 1979-12-14 | 1986-03-20 | Trocknungs-Anlagen-Gesellschaft mbH, 1000 Berlin | Process for making dry food products from cassava roots |
-
2004
- 2004-06-09 NL NL1026370A patent/NL1026370C2/en not_active IP Right Cessation
-
2005
- 2005-05-30 PL PL05749454.4T patent/PL1761567T5/en unknown
- 2005-05-30 EP EP05749454.4A patent/EP1761567B2/en not_active Not-in-force
- 2005-05-30 AT AT05749454T patent/ATE526346T1/en not_active IP Right Cessation
- 2005-05-30 DK DK05749454.4T patent/DK1761567T4/en active
- 2005-05-30 CN CNA2005800181218A patent/CN1964991A/en active Pending
- 2005-05-30 WO PCT/NL2005/000393 patent/WO2005121183A1/en not_active Application Discontinuation
Non-Patent Citations (1)
Title |
---|
See references of WO2005121183A1 * |
Also Published As
Publication number | Publication date |
---|---|
EP1761567B2 (en) | 2016-06-15 |
DK1761567T4 (en) | 2016-09-12 |
ATE526346T1 (en) | 2011-10-15 |
WO2005121183A1 (en) | 2005-12-22 |
PL1761567T3 (en) | 2012-02-29 |
DK1761567T3 (en) | 2012-01-16 |
EP1761567B1 (en) | 2011-09-28 |
PL1761567T5 (en) | 2016-12-30 |
CN1964991A (en) | 2007-05-16 |
EP1761567B9 (en) | 2012-03-07 |
NL1026370C2 (en) | 2005-12-12 |
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